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Exergy analysis of a hydrogen fired combined cycle with natural gas reforming and membrane assisted shift reactors for CO2 capture

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dc.contributor.author Atsonios, K en
dc.contributor.author Panopoulos, KD en
dc.contributor.author Doukelis, A en
dc.contributor.author Koumanakos, A en
dc.contributor.author Kakaras, E en
dc.date.accessioned 2014-03-01T02:53:38Z
dc.date.available 2014-03-01T02:53:38Z
dc.date.issued 2012 en
dc.identifier.issn 01968904 en
dc.identifier.uri https://dspace.lib.ntua.gr/xmlui/handle/123456789/36460
dc.subject Aspen plus en
dc.subject CCS en
dc.subject Exergy en
dc.subject Hydrogen en
dc.subject Membrane reactor en
dc.subject Reforming en
dc.subject Shift en
dc.subject.other A-carbon en
dc.subject.other ASPEN PLUS en
dc.subject.other Autothermal reforming en
dc.subject.other CCS en
dc.subject.other Combined cycle en
dc.subject.other Exergetic analysis en
dc.subject.other Exergy Analysis en
dc.subject.other Hydrogen delivery en
dc.subject.other Membrane reactor en
dc.subject.other Natural Gas Reforming en
dc.subject.other Operating parameters en
dc.subject.other Optimal power en
dc.subject.other Reactor systems en
dc.subject.other Reactor temperatures en
dc.subject.other Shift en
dc.subject.other Steam-to-carbon ratio en
dc.subject.other Water gas shift reactors en
dc.subject.other Bioreactors en
dc.subject.other Exergy en
dc.subject.other Fossil fuels en
dc.subject.other Hydrogen en
dc.subject.other Hydrogen production en
dc.subject.other Industrial applications en
dc.subject.other Natural gas en
dc.subject.other Reforming reactions en
dc.subject.other Water gas shift en
dc.subject.other Carbon dioxide en
dc.title Exergy analysis of a hydrogen fired combined cycle with natural gas reforming and membrane assisted shift reactors for CO2 capture en
heal.type conferenceItem en
heal.identifier.primary 10.1016/j.enconman.2012.02.015 en
heal.identifier.secondary http://dx.doi.org/10.1016/j.enconman.2012.02.015 en
heal.publicationDate 2012 en
heal.abstract Hydrogen production from fossil fuels together with carbon capture has been suggested as a means of providing a carbon free power. The paper presents a comparative exergetic analysis performed on the hydrogen production from natural gas with several combinations of reactor systems: (a) oxy or air fired autothermal reforming with subsequent water gas shift reactor and (b) membrane reactor assisted with shift catalysts. The influence of reactor temperature and pressure as well as operating parameter steam-to-carbon ratio, is also studied exergetically. The results indicate optimal power plant configurations with CO2 capture, or hydrogen delivery for industrial applications. © 2012 Elsevier Ltd. All rights reserved. en
heal.journalName Energy Conversion and Management en
dc.identifier.doi 10.1016/j.enconman.2012.02.015 en
dc.identifier.volume 60 en
dc.identifier.spage 196 en
dc.identifier.epage 203 en


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